CN106972183B - Nanometer PPy-Au modified metal double polar plates of polymer electrolyte film fuel cell and preparation method thereof - Google Patents
Nanometer PPy-Au modified metal double polar plates of polymer electrolyte film fuel cell and preparation method thereof Download PDFInfo
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- 229910052751 metal Inorganic materials 0.000 title claims abstract description 56
- 239000002184 metal Substances 0.000 title claims abstract description 56
- 239000000446 fuel Substances 0.000 title claims abstract description 32
- 239000005518 polymer electrolyte Substances 0.000 title claims abstract description 27
- 238000002360 preparation method Methods 0.000 title claims abstract description 12
- 239000012528 membrane Substances 0.000 claims abstract description 29
- 238000000034 method Methods 0.000 claims abstract description 21
- 239000000758 substrate Substances 0.000 claims abstract description 19
- 239000008151 electrolyte solution Substances 0.000 claims abstract description 16
- 230000007797 corrosion Effects 0.000 claims abstract description 12
- 238000005260 corrosion Methods 0.000 claims abstract description 12
- 238000001308 synthesis method Methods 0.000 claims abstract description 5
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 claims description 27
- KAESVJOAVNADME-UHFFFAOYSA-N Pyrrole Chemical compound C=1C=CNC=1 KAESVJOAVNADME-UHFFFAOYSA-N 0.000 claims description 24
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 10
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 10
- 229910001220 stainless steel Inorganic materials 0.000 claims description 10
- 235000006408 oxalic acid Nutrition 0.000 claims description 9
- 239000011159 matrix material Substances 0.000 claims description 7
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 5
- 229910003460 diamond Inorganic materials 0.000 claims description 5
- 239000010432 diamond Substances 0.000 claims description 5
- ZOMNIUBKTOKEHS-UHFFFAOYSA-L dimercury dichloride Chemical class Cl[Hg][Hg]Cl ZOMNIUBKTOKEHS-UHFFFAOYSA-L 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- 229910052697 platinum Inorganic materials 0.000 claims description 5
- 239000000243 solution Substances 0.000 claims description 5
- 230000015572 biosynthetic process Effects 0.000 claims description 4
- 230000004048 modification Effects 0.000 claims description 4
- 238000012986 modification Methods 0.000 claims description 4
- 238000003786 synthesis reaction Methods 0.000 claims description 4
- 229910000963 austenitic stainless steel Inorganic materials 0.000 claims description 2
- 238000004821 distillation Methods 0.000 claims description 2
- 229910001039 duplex stainless steel Inorganic materials 0.000 claims description 2
- 229910004042 HAuCl4 Inorganic materials 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- 230000008569 process Effects 0.000 abstract description 6
- 238000005457 optimization Methods 0.000 abstract 1
- 230000001360 synchronised effect Effects 0.000 abstract 1
- 210000004027 cell Anatomy 0.000 description 25
- 239000010935 stainless steel Substances 0.000 description 8
- 239000004519 grease Substances 0.000 description 4
- 238000004506 ultrasonic cleaning Methods 0.000 description 4
- 239000010964 304L stainless steel Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 229910045601 alloy Inorganic materials 0.000 description 3
- 239000000956 alloy Substances 0.000 description 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 3
- 229910002804 graphite Inorganic materials 0.000 description 3
- 239000010439 graphite Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000007769 metal material Substances 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 238000002161 passivation Methods 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 229920000128 polypyrrole Polymers 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- LDMOEFOXLIZJOW-UHFFFAOYSA-N 1-dodecanesulfonic acid Chemical compound CCCCCCCCCCCCS(O)(=O)=O LDMOEFOXLIZJOW-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000007772 electroless plating Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 238000006056 electrooxidation reaction Methods 0.000 description 1
- 238000009713 electroplating Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 238000002715 modification method Methods 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 150000004767 nitrides Chemical class 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 210000002381 plasma Anatomy 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 230000007847 structural defect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0223—Composites
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/34—Pretreatment of metallic surfaces to be electroplated
- C25D5/36—Pretreatment of metallic surfaces to be electroplated of iron or steel
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D9/00—Electrolytic coating other than with metals
- C25D9/02—Electrolytic coating other than with metals with organic materials
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0206—Metals or alloys
- H01M8/0208—Alloys
- H01M8/021—Alloys based on iron
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0221—Organic resins; Organic polymers
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M2008/1095—Fuel cells with polymeric electrolytes
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Abstract
本发明提供一种纳米PPy‑Au改性的聚合物电解质膜燃料电池金属双极板的制备方法,采用电化学合成法,将金属基体置于电解质溶液中,于温度25℃,电流4mA/cm2,超声频率24kHz,时间10~30min条件下进行改性层合成。采用本发明提供方法制备的双极板,金属基体表面为2~5μm的纳米PPy‑Au改性层,腐蚀速度低于6μA/cm2,接触电阻低于10mΩ·cm2。在不影响强度的前提下,本发明提供的方法能实现金属双极板耐蚀性和表面导电性的同步优化,进而达到提高聚合物电解质膜燃料电池性能的目的。该制备方法具有设备和工艺简单、成本低廉等优点,能实现双极板规模批量生产。The invention provides a method for preparing a metal bipolar plate of a polymer electrolyte membrane fuel cell modified by nanometer PPy-Au. The electrochemical synthesis method is used to place the metal substrate in the electrolyte solution at a temperature of 25°C and a current of 4mA/cm 2. Synthesize the modified layer under the conditions of ultrasonic frequency 24kHz and time 10-30min. The bipolar plate prepared by the method provided by the invention has a 2-5 μm nanometer PPy-Au modified layer on the surface of the metal substrate, the corrosion rate is lower than 6 μA/cm 2 , and the contact resistance is lower than 10 mΩ·cm 2 . On the premise of not affecting the strength, the method provided by the invention can realize the synchronous optimization of the corrosion resistance and surface conductivity of the metal bipolar plate, thereby achieving the purpose of improving the performance of the polymer electrolyte membrane fuel cell. The preparation method has the advantages of simple equipment and process, low cost and the like, and can realize mass production of bipolar plates.
Description
技术领域technical field
本发明属于燃料电池技术领域。特别涉及聚合物电解质膜燃料电池金属双极板及其表面改性。The invention belongs to the technical field of fuel cells. In particular, it relates to metal bipolar plates of polymer electrolyte membrane fuel cells and their surface modification.
背景技术Background technique
聚合物电解质膜燃料电池具有能量转化效率高、寿命长、工作温度低、环境友好和低温快速启动等特点,是一种军民通用的可移动电源,尤其适合建设分散电站和用作交通运输工具的动力源。然而,相对较高的成本、重量和体积等诸多因素在很大程度上限制了聚合物电解质膜燃料电池的规模商业化生产和应用。因此,降低其各组件材料和制备成本一直是各国政府和研究者关注和急待解决的热点问题。Polymer electrolyte membrane fuel cells have the characteristics of high energy conversion efficiency, long life, low operating temperature, environmental friendliness, and low-temperature rapid start-up. power source. However, many factors such as relatively high cost, weight, and volume largely limit the large-scale commercial production and application of polymer electrolyte membrane fuel cells. Therefore, reducing the cost of materials and preparation of its various components has always been a hot issue that governments and researchers pay attention to and urgently need to solve.
作为聚合物电解质膜燃料电池的多功能组件之一,双极板的功能主要包括分隔反应气体、集流导电、支撑膜电极、为反应气体提供通道并使其分布均匀、方便电池组的水热管理。石墨具有良好的导电性和化学稳定性,是一种理想的聚合物电解质膜燃料电池双极板材料。然而,高脆性、低强度以及结构疏松多孔等不足使其难以生产低重量、低体积的高性能燃料电池组。此外,在石墨板表面加工流场时所需工艺复杂且费用高昂,约占聚合物电解质膜燃料电池总成本的80%左右。与传统石墨相比,金属材料在强韧性、导电性和气密性等方面具有明显优势。值得注意的是,可以采用机械加工和冲压的方法在金属表面加工各种形状的流场,尤其适合于批量生产,能够大幅度提高聚合物电解质膜燃料电池的质量比功率和体积比功率。目前常用的金属双极板材料主要包括铁基合金、镍基合金和铝、钛及其合金等。As one of the multifunctional components of the polymer electrolyte membrane fuel cell, the functions of the bipolar plate mainly include separating the reactant gas, collecting and conducting electricity, supporting the membrane electrode, providing channels for the reactant gas and making it evenly distributed, and facilitating the hydrothermal of the battery pack. manage. Graphite has good electrical conductivity and chemical stability, and is an ideal bipolar plate material for polymer electrolyte membrane fuel cells. However, the shortcomings of high brittleness, low strength, and porous structure make it difficult to produce low-weight, low-volume high-performance fuel cell stacks. In addition, the process required to process the flow field on the surface of the graphite plate is complex and expensive, accounting for about 80% of the total cost of the polymer electrolyte membrane fuel cell. Compared with traditional graphite, metal materials have obvious advantages in terms of strength, toughness, electrical conductivity, and air tightness. It is worth noting that machining and stamping methods can be used to process various shapes of flow fields on the metal surface, which is especially suitable for mass production and can greatly improve the mass specific power and volume specific power of polymer electrolyte membrane fuel cells. Currently commonly used metal bipolar plate materials mainly include iron-based alloys, nickel-based alloys, aluminum, titanium and their alloys.
受质子交换膜部分降解和电极制备工艺特殊性的影响,在聚合物电解质膜燃料电池的工作环境中常存在SO4 2-、SO3 2-、CO3 2-、HSO4 -和HSO3 -等离子。因此,金属双极板在这种酸性条件下发生电化学腐蚀是不可避免的。尽管金属双极板表面所形成的钝化膜能够有效抑制金属进一步腐蚀,但钝化膜中金属氧化物的半导体性质会导致表面导电性降低。显然,所有这些因素势必造成一些电能的消耗和燃料电池组输出功率的降低,从而影响电池组的耐久性。为了同时满足其在导电性和耐蚀性上的要求,在金属双极板表面制备改性层不失为一种有效方法,这对聚合物电解质膜燃料电池的发展和应用必将产生重要影响。显然,价格高昂的贵金属改性层不适于生产低成本的电池组。受制备工艺条件的限制,采用PVD、CVD、化学镀和电镀等不同的方法制备的氮化物和氧化物改性层常存在难以避免的微孔和微裂纹等组织缺陷。这些缺陷无疑会引起金属双极板局部腐蚀并导致改性层剥落,从而明显缩短聚合物电解质膜燃料电池的使用寿命。基于现有表面改性方法总是存在或多或少的足限性,还没有任何一种通过表面改性处理的金属双极板能够满足目前聚合物电解质膜燃料电池规模化市场应用的要求。因此,发展成本低廉、高表面导电性和耐蚀性的双极板仍旧是聚合物电解质膜燃料电池的必然途径,也必然对其商业化进程产生重要的影响。Affected by the partial degradation of the proton exchange membrane and the particularity of the electrode preparation process, SO 4 2- , SO 3 2- , CO 3 2- , HSO 4 - and HSO 3 - plasmas often exist in the working environment of polymer electrolyte membrane fuel cells . Therefore, electrochemical corrosion of metal bipolar plates under such acidic conditions is inevitable. Although the passivation film formed on the surface of the metal bipolar plate can effectively inhibit the further corrosion of the metal, the semiconductor properties of the metal oxide in the passivation film will lead to a decrease in surface conductivity. Apparently, all these factors are bound to cause some electric energy consumption and a reduction in the output power of the fuel cell stack, thereby affecting the durability of the battery pack. In order to meet the requirements of electrical conductivity and corrosion resistance at the same time, it is an effective method to prepare a modified layer on the surface of the metal bipolar plate, which will have an important impact on the development and application of polymer electrolyte membrane fuel cells. Obviously, the expensive noble metal modification layer is not suitable for the production of low-cost battery packs. Limited by the preparation process conditions, the nitride and oxide modified layers prepared by different methods such as PVD, CVD, electroless plating and electroplating often have unavoidable micropores and microcracks and other structural defects. These defects will undoubtedly cause localized corrosion of the metal bipolar plate and lead to peeling off of the modified layer, thereby significantly shortening the service life of the polymer electrolyte membrane fuel cell. Based on the fact that the existing surface modification methods are always more or less insufficient, there is no metal bipolar plate treated by surface modification that can meet the requirements of the current large-scale market application of polymer electrolyte membrane fuel cells. Therefore, the development of low-cost, high-surface conductivity and corrosion-resistant bipolar plates is still an inevitable path for polymer electrolyte membrane fuel cells, and it will inevitably have an important impact on its commercialization process.
发明内容Contents of the invention
本发明目的在于提供一种聚合物电解质膜燃料电池金属双极板表面纳米PPy(聚吡咯)-Au改性层及其制备方法。该方法所需设备简单、易于生产加工、成本低廉,能够满足规模化市场应用的要求。The purpose of the invention is to provide a nano PPy (polypyrrole)-Au modified layer on the surface of a metal bipolar plate of a polymer electrolyte membrane fuel cell and a preparation method thereof. The method requires simple equipment, is easy to produce and process, and has low cost, and can meet the requirements of large-scale market applications.
本发明提供一种纳米PPy-Au改性的燃料电池双极板的制备方法,以金属材料为基体,表面为纳米PPy-Au改性层。该改性层采用电化学合成方法制备,表面致密,无裂纹,与基体紧密结合。表面改性后的金属双极板能够显著提高聚合物电解质膜燃料电池的输出功率和使用寿命。The invention provides a method for preparing a nano PPy-Au modified fuel cell bipolar plate, which uses a metal material as a matrix and a nano PPy-Au modified layer on the surface. The modified layer is prepared by an electrochemical synthesis method, and has a dense surface without cracks and is closely combined with the matrix. The surface-modified metal bipolar plate can significantly improve the output power and service life of the polymer electrolyte membrane fuel cell.
为了实现上述目的,本发明提供的聚合物电解质膜燃料电池金属双极板采用以下技术方法制备:In order to achieve the above object, the polymer electrolyte membrane fuel cell metal bipolar plate provided by the present invention is prepared by the following technical methods:
采用电化学合成法,先将金属基体置于电解质溶液中进行改性层合成,温度为25℃,电流为4mA/cm2,超声频率为24kHz,时间为10~30min;上述条件可以更好的使吡咯氧化和HAuCl4还原;在进行改性层合成前,金属基体要按照以下步骤进行预处理:金属基体经400~2500#砂纸依次打磨、金刚石研磨膏抛光。为了除去其表面油脂和污染物,依次用丙酮、酒精溶液进行超声波清洗,时间为15min;Using the electrochemical synthesis method, first put the metal substrate in the electrolyte solution to synthesize the modified layer, the temperature is 25°C, the current is 4mA/cm 2 , the ultrasonic frequency is 24kHz, and the time is 10-30min; the above conditions can be better Oxidize pyrrole and reduce HAuCl 4 ; before synthesizing the modified layer, the metal substrate should be pretreated according to the following steps: the metal substrate is sequentially polished with 400-2500 # sandpaper, and polished with diamond abrasive paste. In order to remove the grease and pollutants on the surface, ultrasonic cleaning is performed with acetone and alcohol solution for 15 minutes;
所述电化学合成法采用三电极体系:金属铂片作为辅助电极、饱和甘汞电极作为参比电极、金属基体作为工作电极;The electrochemical synthesis method adopts a three-electrode system: a metal platinum sheet is used as an auxiliary electrode, a saturated calomel electrode is used as a reference electrode, and a metal matrix is used as a working electrode;
所述电解质溶液由0.1mol/L乙二酸、0.1mol/L吡咯单体、100ppm DBSA(十二烷基磺酸)和3~10ppm HAuCl4组成;电解质溶液按照以下顺序配制:先将乙二酸和DBSA混合均匀,再加入蒸馏提纯的吡咯,最后加入HAuCl4。The electrolyte solution is composed of 0.1mol/L oxalic acid, 0.1mol/L pyrrole monomer, 100ppm DBSA (dodecylsulfonic acid) and 3-10ppm HAuCl 4 ; the electrolyte solution is prepared in the following order: first diethylene glycol Mix the acid and DBSA evenly, then add pyrrole purified by distillation, and finally add HAuCl 4 .
本发明提供的上述方法中,所述金属基体材料为不锈钢。进一步的,所述不锈钢包括奥氏体不锈钢、铁素体不锈钢、双相不锈钢。In the above method provided by the present invention, the metal base material is stainless steel. Further, the stainless steel includes austenitic stainless steel, ferritic stainless steel and duplex stainless steel.
采用本发明提供方法制备的聚合物电解质膜燃料电池金属双极由厚度2~5μm的表面纳米PPy-Au改性层和厚度0.1~3mm的金属基体组成。本发明制备的表面纳米PPy-Au复合改性的金属双极板腐蚀速度低于6μA/cm2,接触电阻低于10mΩ·cm2。The polymer electrolyte membrane fuel cell metal bipolar prepared by the method provided by the invention is composed of a surface nanometer PPy-Au modified layer with a thickness of 2-5 μm and a metal matrix with a thickness of 0.1-3 mm. The surface nano PPy-Au composite modified metal bipolar plate prepared by the invention has a corrosion rate lower than 6μA/cm 2 and a contact resistance lower than 10mΩ·cm 2 .
本发明提供的方法制备的金属双极板优点在于:表面纳米PPy-Au改性的金属双极板制备方法所需设备简单,生产工艺成熟,易于实现批量化生产。本发明制备的表面纳米PPy-Au改性的金属双极板,能够同时满足其在耐蚀性和表面导电性等方面的使用要求,可以应用于聚合物电解质膜燃料电池领域,对于加快聚合物电解质膜燃料电池金属双极板的广泛应用具有重要的实际意义。The metal bipolar plate prepared by the method provided by the invention has the advantages that the preparation method of the metal bipolar plate modified by surface nanometer PPy-Au requires simple equipment, mature production technology, and is easy to realize mass production. The surface nano PPy-Au modified metal bipolar plate prepared by the present invention can meet its use requirements in terms of corrosion resistance and surface conductivity at the same time, and can be applied to the field of polymer electrolyte membrane fuel cells. The wide application of metal bipolar plates in electrolyte membrane fuel cells has important practical significance.
具体实施方式Detailed ways
实施例1Example 1
本实施例提供的纳米PPy-Au改性的聚合物电解质膜燃料电池金属双极板,按照以下步骤在AISI 304L不锈钢基体上沉积纳米PPy-Au改性层:The nano PPy-Au modified polymer electrolyte membrane fuel cell metal bipolar plate provided in this example, deposits a nano PPy-Au modified layer on the AISI 304L stainless steel substrate according to the following steps:
1)预处理:AISI 304L不锈钢基体经400~2500#砂纸依次打磨、金刚石研磨膏抛光。为了除去其表面油脂和污染物,依次用丙酮、酒精溶液进行超声波清洗,时间为15min。1) Pretreatment: AISI 304L stainless steel substrate is polished with 400~2500 # sandpaper in sequence, and polished with diamond abrasive paste. In order to remove the grease and pollutants on the surface, ultrasonic cleaning is carried out with acetone and alcohol solution for 15 minutes.
2)电化学合成采用三电极体系:金属铂片、饱和甘汞电极和金属基体分别作为辅助电极、参比电极和工作电极;2) Electrochemical synthesis adopts a three-electrode system: metal platinum sheet, saturated calomel electrode and metal matrix are used as auxiliary electrode, reference electrode and working electrode respectively;
电解质溶液配制:先将乙二酸和DBSA混合均匀,再加入蒸馏提纯的吡咯,最后加入HAuCl4。所述电解质溶液中,乙二酸浓度为0.1M,吡咯浓度为0.1M,DBSA浓度为100ppm,HAuCl4浓度为7ppm。Electrolyte solution preparation: first mix oxalic acid and DBSA evenly, then add distilled and purified pyrrole, and finally add HAuCl 4 . In the electrolyte solution, the concentration of oxalic acid is 0.1M, the concentration of pyrrole is 0.1M, the concentration of DBSA is 100ppm, and the concentration of HAuCl 4 is 7ppm.
3)纳米PPy-Au改性层制备:将预处理的金属基体置于上述配好的电解质溶液中进行改性层合成,温度为25℃,电流为4mA/cm2,超声频率为24kHz,时间为10min。3) Preparation of nano-PPy-Au modified layer: place the pretreated metal substrate in the above prepared electrolyte solution to synthesize the modified layer, the temperature is 25°C, the current is 4mA/cm 2 , the ultrasonic frequency is 24kHz, and the time is 10min.
本实施例制备的纳米PPy-Au改性的AISI 304L不锈钢双极板,改性层厚度为2μm。本发明中纳米PPy-Au改性的金属双极板腐蚀速度低于4.5μA/cm2,接触电阻率低于3mΩ·cm2。The nano-PPy-Au modified AISI 304L stainless steel bipolar plate prepared in this example has a modified layer thickness of 2 μm. The corrosion rate of the nano PPy-Au modified metal bipolar plate in the invention is lower than 4.5μA/cm 2 , and the contact resistivity is lower than 3mΩ·cm 2 .
实施例2:Example 2:
本实施例提供的纳米PPy-Au改性的聚合物电解质膜燃料电池金属双极板,按照以下步骤在AISI 444不锈钢基体上制备纳米PPy-Au改性层:The nano-PPy-Au modified polymer electrolyte membrane fuel cell metal bipolar plate provided in this example is prepared on the AISI 444 stainless steel substrate according to the following steps:
1)预处理:AISI 444不锈钢基体经400~2500#砂纸依次打磨、金刚石研磨膏抛光。为了除去其表面油脂,依次用丙酮、酒精溶液进行超声波清洗,时间为15min。1) Pretreatment: AISI 444 stainless steel substrate is polished with 400~2500 # sandpaper in sequence, and polished with diamond abrasive paste. In order to remove the surface grease, ultrasonic cleaning was performed with acetone and alcohol solution for 15 minutes.
2)电化学合成采用三电极体系:金属铂片、饱和甘汞电极和金属基体分别作为辅助电极、参比电极和工作电极;2) Electrochemical synthesis adopts a three-electrode system: metal platinum sheet, saturated calomel electrode and metal matrix are used as auxiliary electrode, reference electrode and working electrode respectively;
电解质溶液:先将乙二酸和DBSA混合均匀,再加入蒸馏提纯的吡咯,最后加入HAuCl4。所述电解质溶液中,乙二酸浓度为0.1M,吡咯浓度为0.1M,DBSA浓度为100ppm,HAuCl4浓度为5ppm。Electrolyte solution: Mix oxalic acid and DBSA evenly, then add distilled and purified pyrrole, and finally add HAuCl 4 . In the electrolyte solution, the concentration of oxalic acid is 0.1M, the concentration of pyrrole is 0.1M, the concentration of DBSA is 100ppm, and the concentration of HAuCl 4 is 5ppm.
3)纳米PPy-Au改性层制备:将预处理的金属基体置于上述配好的电解质溶液中进行改性层合成,温度为25℃,电流为4mA/cm2,超声频率为24kHz,时间为20min。3) Preparation of nano-PPy-Au modified layer: place the pretreated metal substrate in the above prepared electrolyte solution to synthesize the modified layer, the temperature is 25°C, the current is 4mA/cm 2 , the ultrasonic frequency is 24kHz, and the time is for 20min.
本实施例制备的纳米PPy-Au改性的AISI 444不锈钢双极板,改性层厚度为3.6μm。本发明中纳米PPy-Au改性的金属双极板腐蚀速度低于4μA/cm2,接触电阻率低于5.3mΩ·cm2。The nano PPy-Au modified AISI 444 stainless steel bipolar plate prepared in this example has a modified layer thickness of 3.6 μm. The corrosion rate of the nano PPy-Au modified metal bipolar plate in the invention is lower than 4μA/cm 2 , and the contact resistivity is lower than 5.3mΩ·cm 2 .
实施例3:Embodiment 3:
本实施例提供的纳米PPy-Au改性的聚合物电解质膜燃料电池金属双极板,按照以下步骤在AISI 2205不锈钢基体上制备纳米PPy-Au改性层:The nano PPy-Au modified polymer electrolyte membrane fuel cell metal bipolar plate provided in this example is prepared on the AISI 2205 stainless steel substrate according to the following steps:
1)预处理:AISI 2205不锈钢基体经400~2500#砂纸依次打磨、金刚石研磨膏抛光。为了除去其表面油脂,依次用丙酮、酒精溶液进行超声波清洗,时间为15min。1) Pretreatment: AISI 2205 stainless steel substrate is polished with 400~2500 # sandpaper in sequence, and polished with diamond abrasive paste. In order to remove the surface grease, ultrasonic cleaning was performed with acetone and alcohol solution for 15 minutes.
2)电化学合成采用常用的三电极体系:金属铂片、饱和甘汞电极和金属基体分别作为辅助电极、参比电极和工作电极。2) The commonly used three-electrode system was used for electrochemical synthesis: metal platinum sheet, saturated calomel electrode and metal substrate were used as auxiliary electrode, reference electrode and working electrode, respectively.
电解质溶液:先将乙二酸和DBSA混合均匀,再加入蒸馏提纯的吡咯,最后加入HAuCl4。所述电解质溶液中,乙二酸浓度为0.1M,吡咯浓度为0.1M,DBSA浓度为100ppm,HAuCl4浓度为10ppm。Electrolyte solution: Mix oxalic acid and DBSA evenly, then add distilled and purified pyrrole, and finally add HAuCl 4 . In the electrolyte solution, the concentration of oxalic acid is 0.1M, the concentration of pyrrole is 0.1M, the concentration of DBSA is 100ppm, and the concentration of HAuCl 4 is 10ppm.
3)纳米PPy-Au改性层制备:将预处理的金属基体置于上述配好的电解质溶液中进行改性层合成,温度为25℃。为了使吡咯单体氧化和HAuCl4还原,电流为4mA/cm2,超声频率为24kHz,时间为25min。3) Preparation of nano-PPy-Au modified layer: the pretreated metal substrate was placed in the above prepared electrolyte solution to synthesize the modified layer at a temperature of 25°C. In order to oxidize pyrrole monomer and reduce HAuCl 4 , the current is 4mA/cm 2 , the ultrasonic frequency is 24kHz, and the time is 25min.
本实施例制备的纳米PPy-Au改性的AISI 2205不锈钢双极板,改性层厚度为4.4μm。本发明中纳米PPy-Au改性的金属双极板腐蚀速度低于5μA/cm2,接触电阻率低于8.8mΩ·cm2。The nano PPy-Au modified AISI 2205 stainless steel bipolar plate prepared in this example has a modified layer thickness of 4.4 μm. The corrosion rate of the nano PPy-Au modified metal bipolar plate in the invention is lower than 5μA/cm 2 , and the contact resistivity is lower than 8.8mΩ·cm 2 .
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| CN1787262A (en) * | 2004-12-08 | 2006-06-14 | 中国科学院金属研究所 | Method for surface treating stainless steel double polar plate of proton exchanging film fuel cell |
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| CN102034990A (en) * | 2009-09-25 | 2011-04-27 | 北京有色金属研究总院 | Metallic bipolar plate of proton exchange membrane fuel cell and surface modification method thereof |
| CN102054989A (en) * | 2010-12-06 | 2011-05-11 | 长沙理工大学 | Bipolar plate for proton exchange membrane fuel cell and manufacture method thereof |
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| CN1787262A (en) * | 2004-12-08 | 2006-06-14 | 中国科学院金属研究所 | Method for surface treating stainless steel double polar plate of proton exchanging film fuel cell |
| CN101375442A (en) * | 2005-08-12 | 2009-02-25 | 通用汽车环球科技运作公司 | Fuel cell component having a coating comprising nanoparticles |
| CN101488574A (en) * | 2008-01-16 | 2009-07-22 | 中国科学院金属研究所 | Proton exchange film fuel cell stainless steel bi-polar plate and production thereof |
| CN102034990A (en) * | 2009-09-25 | 2011-04-27 | 北京有色金属研究总院 | Metallic bipolar plate of proton exchange membrane fuel cell and surface modification method thereof |
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